Electrocatalytic oxidation treatment device and method for high-salt industrial wastewater

Abstract

The invention relates to the technical field of sewage treatment, and discloses a high-salt industrial wastewater electrocatalytic oxidation treatment device and method.The device comprises a reaction assembly, the reaction assembly comprises a machine body, a slag scraper is arranged above the machine body, a gas dissolving assembly is arranged on one side of the machine body, and a flow guide assembly is arranged in the machine body; a partition plate is arranged in the machine body, a mounting frame is arranged on one side of the partition plate, an electrode assembly is arranged on the mounting frame, the flow guide assembly comprises a sleeve, the sleeve is arranged on one side of the electrode assembly, a liquid suction pipe is arranged at one end of the sleeve, and a liquid inlet pipe is arranged at the end, away from the liquid suction pipe, of the sleeve. A driving paddle is arranged in the sleeve, and an adjusting assembly is arranged on the surface of the sleeve. The use state of the electrode assembly is monitored in real time, the working state of the adjusting assembly is automatically adjusted according to the monitoring result, automatic control over the wastewater treatment process is achieved, and the wastewater treatment efficiency is improved.

Description

Technical Field

[0001] The invention belongs to the technical field of sewage treatment, and specifically relates to a device and method for electrocatalytic oxidation treatment of high-salt industrial wastewater. Background Art

[0002] High-salt industrial wastewater contains a large amount of salt and organic pollutants. Traditional treatment methods are difficult to effectively remove pollutants and the treatment cost is high. Electrocatalytic oxidation technology has broad application prospects in the treatment of high-salt industrial wastewater due to its advantages such as high efficiency and environmental protection. Electrocatalytic oxidation technology consists of a complete current circuit consisting of a power source, anode and cathode, and a catalyst. The air produces hydroxyl radical intermediates under the action of electric current, and the free radical intermediates react with the organic pollutants in the wastewater as the main oxidant to purify the wastewater. The electrocatalytic oxidation technology for wastewater treatment has multiple functions such as oxidation, reduction, neutralization, and coagulation, and can be applied to a variety of difficult-to-treat wastewaters.

[0003] A Chinese patent with application number 202410308712.3 discloses an electrocatalytic oxidation sewage treatment device, including a box, a plurality of electrolytic electrodes are fixedly connected to the inner wall of the box, a lifting component is installed in the box, and a cleaning component for cleaning dirt is installed on the lifting component; the lifting component includes two guide rods fixedly connected to the bottom surface of the box, both of which are vertically arranged, and both of which are sleeved with floating plates, and both of which can slide vertically along the guide rods, and the tops of the two floating plates are fixedly connected to fixed plates, and the two fixed plates are connected by connecting plates, and the cleaning component is installed on the two fixed plates; both of the floating plates are installed with limiting components for limiting the position between the floating plates and the guide rods. This device solves the problem of poor dirt cleaning effect, but in actual use, suspended matter is prone to accumulation at the bottom of the box, resulting in poor sewage treatment effect.

[0004] Based on the above scheme, since there are more impurities in the wastewater, the impurities are easily attached to the surface of the electrode assembly and form a covering layer on the surface of the electrode assembly for a long time, which hinders the contact between the electrode assembly and the wastewater and reduces the activity and reaction efficiency of the electrode assembly; and since the bubbles are not fully combined with the suspended matter in the wastewater, part of the suspended matter is deposited at the bottom of the body, thereby affecting the impurity removal effect of the wastewater. Summary of the invention

[0005] In view of the above problems, the present invention provides a device and method for electrocatalytic oxidation treatment of high-salt industrial wastewater to solve the problems raised in the above background technology.

[0006] To achieve the above object, the present invention provides the following technical solution: a high-salt industrial wastewater electrocatalytic oxidation treatment device, comprising a reaction component, the reaction component comprising a body, a scraper is arranged above the body, a gas dissolving component is arranged on one side of the body, and a flow guide component is arranged inside the body; A partition is provided inside the body, a mounting frame is provided on one side of the partition, and an electrode assembly is provided on the mounting frame; The guide assembly includes a sleeve, which is arranged on one side of the electrode assembly, a liquid extraction tube is arranged at one end of the sleeve, a liquid inlet tube is arranged at the end of the sleeve away from the liquid extraction tube, a driving paddle is arranged inside the sleeve, and an adjustment assembly is arranged on the surface of the sleeve.

[0007] Preferably, the adjustment assembly includes a support plate, which is arranged on the outer surface of the sleeve, and the outer surface of the sleeve is provided with a collection frame adapted to the support plate, a hydraulic rod is provided at one end of the support plate away from the sleeve, and a movable plate is provided at one end of the hydraulic rod away from the support plate, and push plates are provided at both ends of the movable plate.

[0008] Preferably, the driving paddle includes a driving shaft, a rotating blade is provided at one end of the driving shaft close to the partition, the rotating blade is arranged inside the liquid inlet pipe, a fixing frame is provided on the surface of the driving shaft, and the fixing frame is fixedly connected to the inner wall of the sleeve at one end away from the driving shaft.

[0009] Preferably, a through groove is opened on the surface of the sleeve, and a baffle is arranged inside the through groove, a spring is arranged on the surface of the baffle, and a positioning plate is arranged at one end of the spring away from the baffle, and the positioning plate is fixedly arranged on the surface of the sleeve.

[0010] Preferably, a rotation groove is provided at the position where the sleeve is connected to the liquid extraction tube, an assembly hole is provided at the position where the body is connected to the liquid extraction tube, the liquid inlet tube is fixedly arranged on the partition, and the liquid inlet tube is arranged between the electrode assembly and the sleeve.

[0011] Preferably, a slag collecting trough is provided at one end of the machine body, the slag collecting trough is provided below the scraper, a slag discharge pipe is provided at a position of the machine body corresponding to the slag collecting trough, and the slag discharge pipe penetrates and extends to the interior of the slag collecting trough.

[0012] Preferably, two electrolytic cells are arranged on the mounting frame, and the electrode assembly is arranged inside the electrolytic cell. The electrode assembly includes a cathode electrode plate and an anode electrode plate, and the cathode electrode plate and the anode electrode plate are arranged in the electrolytic cell in a cross-spaced manner.

[0013] Preferably, the gas dissolving component includes a gas dissolving tank, a gas supply pipe is arranged below the gas dissolving tank, a gas dissolving releaser is arranged inside the body, the end of the gas supply pipe away from the gas dissolving tank is connected to the gas dissolving releaser, the gas dissolving releaser is located below the electrode assembly, and a fixing groove is provided at the position where the body is connected to the gas supply pipe.

[0014] The present invention also provides a method for electrocatalytic oxidation treatment of high-salt industrial wastewater, and the specific method steps are as follows: S1: First, the wastewater to be treated is passed into the interior of the reaction component, and then the wastewater is electrolyzed through the electrode assembly inside the body. At the same time, the dissolved oxygen content of the wastewater is increased by setting a dissolved gas component to improve the rate of electrocatalytic oxidation; S2: Then, a flow guide component is provided to guide the liquid treated by the electrode component, and stirring is performed during the flow guide process, thereby improving the mixing reaction effect; S3: Finally, the bubbles generated during the electrolytic reaction of the electrode assembly and the bubbles generated by the dissolved gas assembly combine with the suspended solids in the wastewater and float to the liquid surface. The scum on the liquid surface is then cleaned by a scraper to separate the impurities in the wastewater.

[0015] Compared with the prior art, the present invention has the following beneficial effects: 1. The present invention uses the synergistic effect of the sleeve, liquid extraction pipe, liquid inlet pipe and driving paddle of the guide assembly and the regulating assembly to stir and guide the wastewater in the electrolytic cell inside the sleeve, increase the contact opportunity between bubbles and suspended matter, improve the combination effect of bubbles and suspended matter, and thus improve the flotation efficiency.

[0016] 2. The present invention controls the relative position of the baffle and the through slot by adjusting the hydraulic rod, movable plate and push plate of the assembly, thereby increasing the fluidity of the liquid, cleaning impurities on the surface of the electrode assembly, reducing impurity adhesion, and improving the activity and reaction efficiency of the electrode assembly.

[0017] 3. The present invention collects the liquid and suspended matter at the bottom of the flotation tank into a sealed cavity by adjusting the different working states of the components, and combines them with new bubbles again, so that the suspended matter after the secondary combination floats to the liquid surface under the action of the bubbles, reducing the residue of uncombined suspended matter in the water, and avoiding the accumulation of suspended matter at the bottom of the body, which affects the impurity removal effect of the wastewater. BRIEF DESCRIPTION OF THE DRAWINGS

[0018] Figure 1 It is a schematic diagram of the overall structure of the present invention from a first viewing angle; Figure 2 It is a schematic diagram of the overall structure of the present invention from a second viewing angle; Figure 3 For the present invention Figure 2 A magnified image of point A; Figure 4It is a schematic diagram of the partial internal structure of the machine body of the present invention; Figure 5 This is a schematic diagram of the structure of the flow guide assembly of the present invention; Figure 6 This is a schematic diagram of the assembly structure of the sleeve and the driving propeller of the present invention; Figure 7 For the present invention Figure 6 Enlarged view of point B.

[0019] In the figure: 1. reaction component; 101. machine body; 102. partition; 103. slag collecting trough; 104. slag discharge pipe; 105. mounting frame; 106. electrode component; 2. dissolved gas component; 201. dissolved gas tank; 202. gas transmission pipe; 203. dissolved gas releaser; 3. guide component; 301. sleeve; 3011. positioning plate; 3012. baffle; 302. liquid extraction pipe; 303. liquid inlet pipe; 304. driving paddle; 3041. driving shaft; 3042. rotating blade; 3043. fixing frame; 305. supporting plate; 306. hydraulic rod; 307. movable plate; 308. collecting frame; 309. pushing plate; 4. scraper. DETAILED DESCRIPTION

[0020] The following will be combined with the drawings in the embodiments of the present invention to clearly and completely describe the technical solutions in the embodiments of the present invention. Obviously, the described embodiments are only part of the embodiments of the present invention, not all of the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of the present invention.

[0021] like Figures 1 to 7 As shown, a high-salt industrial wastewater electrocatalytic oxidation treatment device of the present invention includes a reaction component 1, the reaction component 1 includes a body 101, a scraper 4 is arranged above the body 101, a gas dissolving component 2 is arranged on one side of the body 101, and a guide component 3 is arranged inside the body 101.

[0022] like Figures 2 to 4 As shown, a partition 102 is provided inside the machine body 101, a mounting frame 105 is provided on one side of the partition 102, an electrode assembly 106 is provided on the mounting frame 105, a slag collecting trough 103 is provided at one end of the machine body 101, the slag collecting trough 103 is provided below the scraper 4, a slag discharge pipe 104 is provided at a position of the machine body 101 corresponding to the slag collecting trough 103, the slag discharge pipe 104 penetrates and extends to the inside of the slag collecting trough 103, and the slag collecting trough 103 and the slag discharge pipe 104 are provided to conveniently collect and discharge the slag generated during the processing.

[0023] Two electrolytic cells are arranged on the mounting frame 105 , and the electrode assembly 106 is arranged inside the electrolytic cell. The electrode assembly 106 includes a cathode electrode plate and an anode electrode plate, and the cathode electrode plate and the anode electrode plate are arranged in the electrolytic cell in a cross-spaced manner.

[0024] The dissolved gas component 2 includes a dissolved gas tank 201, an air supply pipe 202 is arranged below the dissolved gas tank 201, a dissolved gas releaser 203 is arranged inside the body 101, and the end of the air supply pipe 202 away from the dissolved gas tank 201 is connected to the dissolved gas releaser 203, and the dissolved gas releaser 203 is located below the electrode assembly 106. A fixed groove is provided at the position where the body 101 is connected to the air supply pipe 202. The dissolved gas component 2 can release tiny bubbles into the wastewater, increase the dissolved oxygen content of the wastewater, and further improve the efficiency of electrocatalytic oxidation.

[0025] like Figures 5 to 7 As shown, the guide assembly 3 includes a sleeve 301, which is arranged on one side of the electrode assembly 106, a liquid extraction tube 302 is arranged at one end of the sleeve 301, a liquid inlet tube 303 is arranged at the end of the sleeve 301 away from the liquid extraction tube 302, a driving paddle 304 is arranged inside the sleeve 301, the driving paddle 304 includes a driving shaft 3041, a rotating blade 3042 is arranged at one end of the driving shaft 3041 close to the partition 102, the rotating blade 3042 is arranged inside the liquid inlet tube 303, a fixing frame 3043 is arranged on the surface of the driving shaft 3041, and the end of the fixing frame 3043 away from the driving shaft 3041 is fixedly connected to the inner wall of the sleeve 301.

[0026] A rotating groove is provided at the position where the sleeve 301 and the liquid extraction tube 302 are connected, an assembly hole is provided at the position where the body 101 and the liquid extraction tube 302 are connected, and the liquid inlet tube 303 is fixedly arranged on the partition 102, and the liquid inlet tube 303 is arranged between the electrode assembly 106 and the sleeve 301.

[0027] A through groove is provided on the surface of the sleeve 301 , and a baffle 3012 is arranged inside the through groove. A spring is provided on the surface of the baffle 3012 , and a positioning plate 3011 is provided on one end of the spring away from the baffle 3012 . The positioning plate 3011 is fixedly arranged on the surface of the sleeve 301 .

[0028] An adjustment component is provided on the surface of the sleeve 301, and the adjustment component includes a support plate 305, the support plate 305 is provided on the outer surface of the sleeve 301, and the outer surface of the sleeve 301 is provided with a collection frame 308 adapted to the support plate 305, and a hydraulic rod 306 is provided at one end of the support plate 305 away from the sleeve 301, and a movable plate 307 is provided at one end of the hydraulic rod 306 away from the support plate 305, and push plates 309 are provided at both ends of the movable plate 307. Under the action of the hydraulic rod 306, the support plate 305 drives the push plate 309 to squeeze the baffle 3012, so that the baffle 3012 is misaligned with the through groove on the sleeve 301.

[0029] During use, it was found that due to the presence of more impurities in the wastewater, the impurities are easily attached to the surface of the electrode assembly 106, and a covering layer is formed on the surface of the electrode assembly 106 for a long time, which hinders the contact between the electrode assembly 106 and the wastewater, and reduces the activity and reaction efficiency of the electrode assembly 106; and because the bubbles are not fully combined with the suspended matter in the wastewater, part of the suspended matter is deposited at the bottom of the body 101, thereby affecting the impurity removal effect of the wastewater.

[0030] When in use, the interior of the body 101 is divided into an electrolytic cell and an air flotation tank by setting a partition 102, and then the wastewater to be treated is introduced into the interior of the reaction component 1, and the wastewater is electrolyzed by the electrode component 106. The cathode electrode plate in the electrode component 106 is the cathode, and the anode electrode plate in the electrode component 106 is the anode. The wastewater generates a large number of tiny hydrogen bubbles in the cathode state. The diameter of the hydrogen bubbles is generally 18 to 90 microns, which plays the role of an air flotation aid. At the same time, the hydroxide ionized in the anode state plays the role of a coagulant, which helps the impurities in the wastewater to float. Under the action of the water flow, the wastewater in the electrolytic cell enters the air flotation tank through the guide component 3, and then the suspended matter in the wastewater adheres to the microbubbles, floats to the liquid surface with the bubbles and forms a scum layer, and then the scum on the liquid surface is cleaned by the scraper 4, thereby separating the impurities in the wastewater, thereby achieving the effect of purifying the wastewater.

[0031] In order to improve the reaction effect, the gas in the dissolved gas tank 201 is transported to the dissolved gas releaser 203 through the gas delivery pipe 202. Under the action of the dissolved gas releaser 203, the released gas will form tiny bubbles, which float up and pass through the electrode assembly 106, thereby combining with the impurities on the surface of the electrode assembly 106 and floating up, thereby reducing the impurities adhering to the surface of the electrode assembly 106. In the initial state, the controller controls and adjusts the working state of the adjustment components on the surface of the sleeve 301 respectively. Specifically, the controller controls the hydraulic rod 306 to contract, and the hydraulic rod 306 drives the movable plate 307 and the push plate 309 to squeeze the baffle 3012. In this process, the spring is stretched, the baffle 3012 is misaligned with the through slot on the sleeve 301, and at this time, the movable plate 307 and the collection frame 308 are spaced apart. There is a gap, and it is not in a sealed state. Turn on the water pump, and under the action of the water pump, the liquid extraction pipe 302 is sucked, so that the wastewater with bubbles in the electrolytic cell enters the interior of the sleeve 301 through the liquid inlet pipe 303, and the rotating blade 3042 rotates under the action of water force, and then the rotating blade 3042 drives the driving shaft 3041, the fixing frame 3043 and the sleeve 301 to rotate together. During the rotation of the sleeve 301, the wastewater inside the sleeve 301 flows out from the through grooves, that is, the liquid inside the sleeve 301 flows out from the three through grooves respectively, and finally flows to the flotation tank through the gaps between the movable plate 307 and the collecting frame 308 on the adjusting component respectively, thereby realizing the dual functions of diversion and stirring, improving the distribution of bubbles in the flotation tank, and improving the combination effect of bubbles and suspended matter.

[0032] It is worth mentioning that an electrochemical sensor is provided on the electrode assembly 106. When impurities are attached to the surface of the electrode assembly 106, the resistance of the surface of the electrode assembly 106 increases, and the electrocatalytic efficiency is reduced, that is, the conductivity of the electrode assembly 106 decreases. The usage status of the electrode assembly 106 can be obtained through the detection result of the electrochemical sensor.

[0033] If the detection result of the electrochemical sensor shows that the conductivity of the electrode assembly 106 is within the standard range and the conductivity of the electrode assembly 106 is on a downward trend, it indicates that a small amount of impurities are adhered to the surface of the electrode assembly 106. At this time, the controller controls and adjusts the working state of one of the adjustment components on the surface of the sleeve 301. Specifically, the controller controls the hydraulic rod 306 to continue to contract, and the hydraulic rod 306 drives the movable plate 307 to move toward the direction close to the support plate 305, so that the movable plate 307 and the collection frame 308 are in a sealed state. In this process, the movable plate 307 and the push plate 309 The baffle 3012 is squeezed, the spring is stretched, and the opening between the baffle 3012 and the through groove on the sleeve 301 increases. At this time, part of the liquid inside the sleeve 301 enters the sealed cavity surrounded by the movable plate 307 and the collecting frame 308 from the opening between the baffle 3012 and the through groove on the sleeve 301, thereby increasing the amount of liquid entering the sleeve 301. Under the action of the liquid extraction tube 302, the flow rate of the liquid in the electrolytic cell entering the liquid inlet tube 303 is also increased, thereby enhancing the fluidity of the liquid at the position of the electrode assembly 106, and cleaning the impurities adhering to the electrode assembly 106 under the action of the water flow.

[0034] At the same time, the impact force of the liquid on the rotating blade 3042 increases, thereby increasing the rotation speed of the rotating blade 3042, so that the bubbles and suspended matter in the electrolytic cell can be stirred and broken, thereby increasing the contact area between the bubbles and the suspended matter, and also preventing the large volume of the suspended matter from affecting the normal operation of the liquid inlet pipe 303, and further preventing the suspended matter from accumulating at the bottom of the body 101 due to its excessive volume.

[0035] When it is necessary to clean the suspended matter accumulated at the bottom, the controller first controls the working state of another adjusting component on the surface of the sleeve 301. At this time, the three adjusting components on the surface of the sleeve 301 are in different working states. Specifically, the controller first controls the hydraulic rod 306 to extend, and the hydraulic rod 306 drives the movable plate 307 to move away from the support plate 305. At this time, the push plate 309 moves with the movable plate 307. Under the action of the spring, the baffle 3012 moves towards the direction close to the positioning plate 3011, so that the baffle 3012 can press the sleeve 3011. 01 is sealed. When the adjusting component rotates to the lowest point along with the sleeve 301, that is, the distance between the adjusting component and the bottom of the machine body 101 is the shortest, then the controller controls the hydraulic rod 306 to quickly contract, and the hydraulic rod 306 drives the movable plate 307 to move toward the direction close to the support plate 305, so that the movable plate 307 and the collection frame 308 are in a sealed state, and the hydraulic rod 306 drives the movable plate 307 and the push plate 309 to squeeze the baffle 3012, the spring is stretched, and the baffle 3012 is misaligned with the through slot on the sleeve 301. In this process, the movable plate 307 and the collection frame 308 are in a sealed state. The movable plate 307 drives the liquid at the bottom of the flotation tank and collects it into the sealed cavity surrounded by the movable plate 307 and the collection frame 308, and the suspended matter at the bottom of the flotation tank enters the sealed cavity surrounded by the movable plate 307 and the collection frame 308 along with the liquid, and then the liquid in the sealed cavity enters the interior of the sleeve 301 through the gap between the through groove and the baffle 3012, and the uncombined suspended matter at the bottom of the flotation tank and the new bubbles in the sleeve 301 are combined again, increasing the contact opportunity between the bubbles and the suspended matter, and then the wastewater inside the sleeve 301 is discharged from another regulating component position. The suspended matter flows out through the slot at the location where the water is placed, and finally flows into the flotation tank through the gap between the movable plate 307 and the collecting frame 308. The suspended matter after the secondary combination floats to the liquid surface under the action of the bubbles, which can significantly improve the flotation efficiency, so that more suspended matter at the bottom of the flotation tank can be adsorbed by the bubbles and float to the liquid surface to form scum, which can more effectively separate the suspended matter and impurities in the water, and also reduce the residue of uncombined suspended matter in the water, thereby improving the clarity and transparency of the water quality. In addition, the secondary combination process makes full use of the bubbles, reduces the waste of bubbles, and improves the utilization efficiency of resources.

[0036] It is worth noting that an angle sensor is provided on the driving shaft 3041 , and the rotation angle of the adjustment component at different positions of the sleeve 301 can be known through the angle sensor, thereby obtaining the position of the adjustment component.

[0037] By setting an electrochemical sensor to monitor the use status of the electrode assembly 106 in real time, the controller automatically adjusts the working status of the adjustment assembly according to the monitoring results, cleans impurities on the surface of the electrode assembly 106 in time, reduces corrosion and wear of the electrode assembly 106 by impurities, and extends the service life of the electrode assembly 106. By increasing the dissolved oxygen content of the wastewater and optimizing the flotation process, the rate of electrocatalytic oxidation is improved, the automatic control of the wastewater treatment process is realized, and the efficiency and stability of wastewater treatment are improved, thereby improving the activity of the electrode assembly 106, the combination effect of bubbles and suspended matter, the utilization efficiency of resources and the degree of automation of wastewater treatment. Through effective flotation and scraping processes, impurities and suspended matter in the wastewater are separated and collected, reducing the risk of secondary pollution, thereby significantly improving the overall effect of electrocatalytic oxidation treatment of high-salt industrial wastewater, and having significant creativity and practicality.

[0038] The present invention also provides a method for electrocatalytic oxidation treatment of high-salt industrial wastewater, and the specific method steps are as follows: S1: First, the wastewater to be treated is passed into the interior of the reaction component 1, and then the wastewater is electrolyzed by the electrode component 106 inside the body 101, and at the same time, the dissolved oxygen content of the wastewater is increased by setting the gas dissolving component 2 to improve the rate of electrocatalytic oxidation; S2: Then, the liquid treated by the electrode assembly 106 is diverted by setting a diversion assembly 3, and stirred during the diversion process, so as to improve the mixing reaction effect; S3: Finally, the bubbles generated during the electrolytic reaction of the electrode assembly 106 and the bubbles generated by the dissolved gas assembly 2 combine with the suspension in the wastewater and float to the liquid surface, and then the scum on the liquid surface is cleaned by the scraper 4 to separate the impurities in the wastewater.

[0039] It should be noted that, in this article, relational terms such as first and second, etc. are only used to distinguish one entity or operation from another entity or operation, and do not necessarily require or imply any such actual relationship or order between these entities or operations. Moreover, the terms "include", "comprise" or any other variants thereof are intended to cover non-exclusive inclusion, so that a process, method, article or device including a series of elements includes not only those elements, but also other elements not explicitly listed, or also includes elements inherent to such process, method, article or device.

[0040] Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that various changes, modifications, substitutions and variations may be made to the embodiments without departing from the principles and spirit of the present invention, and that the scope of the present invention is defined by the appended claims and their equivalents.

Claims

1. A device for electrocatalytic oxidation treatment of high-salt industrial wastewater, characterized in that: The reaction assembly (1) comprises a machine body (101), a scraper (4) is arranged above the machine body (101), a gas dissolving assembly (2) is arranged on one side of the machine body (101), and a flow guiding assembly (3) is arranged inside the machine body (101); A partition (102) is provided inside the machine body (101), a mounting frame (105) is provided on one side of the partition (102), and an electrode assembly (106) is provided on the mounting frame (105); The flow guide assembly (3) comprises a sleeve (301), the sleeve (301) being arranged on one side of the electrode assembly (106), a liquid extraction tube (302) being arranged at one end of the sleeve (301), a liquid inlet tube (303) being arranged at one end of the sleeve (301) away from the liquid extraction tube (302), a driving paddle (304) being arranged inside the sleeve (301), and an adjustment assembly being arranged on the surface of the sleeve (301).

2. The electrocatalytic oxidation treatment device for high-salt industrial wastewater according to claim 1 is characterized in that: The adjustment assembly comprises a support plate (305), wherein the support plate (305) is arranged on the outer surface of the sleeve (301), and the outer surface of the sleeve (301) is provided with a collection frame (308) adapted to the support plate (305), and a hydraulic rod (306) is arranged at one end of the support plate (305) away from the sleeve (301), and a movable plate (307) is arranged at one end of the hydraulic rod (306) away from the support plate (305), and push plates (309) are arranged at both ends of the movable plate (307).

3. The electrocatalytic oxidation treatment device for high-salt industrial wastewater according to claim 1 is characterized in that: The driving paddle (304) comprises a driving shaft (3041), and a rotating blade (3042) is provided at one end of the driving shaft (3041) close to the partition (102), and the rotating blade (3042) is arranged inside the liquid inlet pipe (303). A fixing frame (3043) is provided on the surface of the driving shaft (3041), and an end of the fixing frame (3043) away from the driving shaft (3041) is fixedly connected to the inner wall of the sleeve (301).

4. The electrocatalytic oxidation treatment device for high-salt industrial wastewater according to claim 1 is characterized in that: A through groove is provided on the surface of the sleeve (301), and a baffle (3012) is arranged inside the through groove. A spring is provided on the surface of the baffle (3012), and a positioning plate (3011) is provided at one end of the spring away from the baffle (3012). The positioning plate (3011) is fixedly arranged on the surface of the sleeve (301).

5. The electrocatalytic oxidation treatment device for high-salt industrial wastewater according to claim 1 is characterized in that: A rotation groove is provided at a position where the sleeve (301) is connected to the liquid extraction tube (302), an assembly hole is provided at a position where the body (101) is connected to the liquid extraction tube (302), the liquid inlet tube (303) is fixedly arranged on the partition (102), and the liquid inlet tube (303) is arranged between the electrode assembly (106) and the sleeve (301).

6. The electrocatalytic oxidation treatment device for high-salt industrial wastewater according to claim 1 is characterized by: A slag collecting trough (103) is provided at one end of the machine body (101), the slag collecting trough (103) is arranged below the slag scraper (4), and a slag discharge pipe (104) is provided at a position of the machine body (101) corresponding to the slag collecting trough (103), the slag discharge pipe (104) penetrates and extends into the interior of the slag collecting trough (103).

7. The electrocatalytic oxidation treatment device for high-salt industrial wastewater according to claim 1 is characterized in that: Two electrolytic cells are arranged on the mounting frame (105), and the electrode assembly (106) is arranged inside the electrolytic cell. The electrode assembly (106) comprises a cathode electrode plate and an anode electrode plate, and the cathode electrode plate and the anode electrode plate are arranged in the electrolytic cell in a cross-spaced manner.

8. The electrocatalytic oxidation treatment device for high-salt industrial wastewater according to claim 1 is characterized by: The gas dissolving component (2) comprises a gas dissolving tank (201), a gas supply pipe (202) is arranged below the gas dissolving tank (201), a gas dissolving releaser (203) is arranged inside the machine body (101), one end of the gas supply pipe (202) away from the gas dissolving tank (201) is connected to the gas dissolving releaser (203), the gas dissolving releaser (203) is located below the electrode component (106), and a fixing groove is provided at a position where the machine body (101) is connected to the gas supply pipe (202).

9. A method for electrocatalytic oxidation treatment of high-salt industrial wastewater, which is achieved by using the electrocatalytic oxidation treatment device for high-salt industrial wastewater as claimed in claim 1, characterized in that: The specific steps are as follows: S1: First, the wastewater to be treated is passed into the interior of the reaction component (1), and then the wastewater is electrolyzed through the electrode component (106) inside the body (101), and at the same time, the dissolved oxygen content of the wastewater is increased by setting the gas dissolving component (2), thereby improving the rate of electrocatalytic oxidation; S2: Then, a flow guiding component (3) is provided to guide the liquid treated by the electrode component (106), and stirring is performed during the flow guiding process, thereby improving the mixing reaction effect; S3: Finally, the bubbles generated during the electrolytic reaction of the electrode assembly (106) and the bubbles generated by the dissolved gas assembly (2) are combined with the suspended solids in the wastewater and float to the liquid surface. The scum on the liquid surface is then cleaned by a scraper (4), thereby separating the impurities in the wastewater.

Images